CN108985643A - The methodology of the heat supply of Gas-steam Combined Cycle cogeneration units and fuel used to generate electricity cost - Google Patents
The methodology of the heat supply of Gas-steam Combined Cycle cogeneration units and fuel used to generate electricity cost Download PDFInfo
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- 238000013139 quantization Methods 0.000 claims abstract description 24
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 10
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- 238000000605 extraction Methods 0.000 claims description 30
- 238000002485 combustion reaction Methods 0.000 claims description 12
- 238000010248 power generation Methods 0.000 claims description 12
- 238000010438 heat treatment Methods 0.000 claims description 9
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 8
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- 239000002918 waste heat Substances 0.000 claims description 5
- 239000003345 natural gas Substances 0.000 claims description 4
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Abstract
The invention discloses the methodologies of a kind of heat supply of Gas-steam Combined Cycle cogeneration units and fuel used to generate electricity cost, for rationally determining for two aspect proportion in fuel cost of heat and generating power.Its technical solution is: it carries out quantification treatment to the utility value of various energy from the angle of different-energy grade, and the energy grade quantization parameter for the heat that steam and flue gas contain is determined by following formula:The present invention has comprehensively considered the thermoelectricity load combination condition in the cascaded utilization of energy relationship and operational process of Gas-steam Combined Cycle under specific operating condition, can reasonable distribution fuel cost to for the aspect of heat and generating power two, provide reference frame to formulate heat supply and generating price.
Description
Technical field
The present invention relates to a kind of reasonable distribution Gas-steam Combined Cycle cogeneration units heat supply and fuel used to generate electricity costs
Method, belong to cogeneration of heat and power technical field.
Background technique
Gas-steam combined cycle system is established on the basis of cascaded utilization of energy, has capacity usage ratio height, the feature of environmental protection
Good advantage.During integrated gas-steam combined cycle power plant, the exhaust gas temperature of gas turbine is often higher, and boiler is needed to return
Waste heat is received, heat loss is reduced.Meanwhile in the cogeneration units of steam circulation, steam first has to enter steam turbine acting guarantor
Generated energy is demonstrate,proved, then some vapor therein, which is just extracted, is supplied to heat user.Therefore join in Gas-steam Combined Cycle thermoelectricity
It produces in unit, electrically and thermally two kinds of energy products are different on energy grade；The heat that the working medium flue gas of combustion gas circulation contains
The working substance steam that grade is higher than steam circulation contains the grade of heat；The heat product that the working substance steam done work into steam turbine contains
Position is higher than the grade for containing heat into the heat-carrying matter steam of heat supply network heat supply.
Since cogeneration units produce the particularity of itself, the thermoelectricity point in cogeneration of heat and power how is rationally and effectively determined
Ratio is spread out, is up to the present still a project that is disputable and being worth discussion.Reasonable cost allocation should be able to be more fully
The actual conditions of conversion, utilization and the loss of energy during reflection cogeneration of heat and power, and reach the reasonable benefit to the energy as far as possible
With.
In traditional cost allocation calculation method, calorimetry is by electric energy and different quality thermal energy equivalent processes, Jin Jincong
It is accounted in terms of the numerical value of energy, and has ignored this key factor of quality, when calculating cost allocation, it is believed that steam power plant
The thermalization power generation part of heat supply does not have cold source and irreversible loss, this partial loss is all utilized to external heat supply.Therefore should
Cold source and irreversible loss are all attributed to heat supply side by method, cannot rationally reflect the practical conversion process of energy in the unit.
The exergey method considers heat supply thermalization steam and does work in steam turbine insufficient influence, paid attention to different pressures,
At a temperature of difference of the heating steam in terms of grade.User's product is encouraged using high-quality high price, the electricity cost allocation method of low-quality low price
Production process is improved in pole, reduces use steam pressure, temperature as far as possible, and to thermalization generated energy is increased, improving steam power plant's economy has rush
Into effect.But the cold source of thermalization power generation part and irreversible loss are all attributed to power generation side by this method, cannot rationally reflect energy
The practical conversion process of amount in the unit.
The exergey method is only usedIt measures the difference of energy in terms of quality, ignores heat user pair completelyApplication.
When turbine discharge parameter and environmental parameter are closer to, sharing for calculating is more close than with actual enthalpy drop method.Therefore,
This method cannot rationally reflect the practical conversion process of energy in the unit.
In view of this, considering simultaneously to overcome the shortcomings of above-mentioned conventional method: in Gas-steam Combined Cycle thermoelectricity
In coproduction unit, electrically and thermally two kinds of energy products are different on energy grade；The heat that the working medium flue gas of combustion gas circulation contains
The working substance steam that amount grade is higher than steam circulation contains the grade of heat；The heat that the working substance steam done work into steam turbine contains
The characteristics of grade contains the grade of heat higher than the heat-carrying matter steam into heat supply network heat supply, the invention proposes a kind of reasonable distributions
The methodology of the heat supply of Gas-steam Combined Cycle cogeneration units and fuel used to generate electricity cost.
Summary of the invention
It is an object of the invention to overcome the deficiencies of the prior art and provide a kind of Gas-steam Combined Cycle thermoelectricity connection
Produce the methodology of unit heat supply and fuel used to generate electricity cost.
Technical scheme is as follows:
The methodology of the heat supply of Gas-steam Combined Cycle cogeneration units and fuel used to generate electricity cost of the invention,
It is characterized in that including the following steps:
1) according to unit practical operation situation, steam Property parameter handbook is consulted, determines the value of parameter needed for calculating, packet
Include environment temperature, enthalpy, entropy and the heating load of each section of heat supply steam extraction, combustion engine and the generated energy of steam turbine etc.；
2) assume that unit shares n sections of heat supply steam extractions, determine the energy grade quantization system for the heat that i-th section of heat supply steam extraction is contained
Several and total heat supply steam extraction energy grade quantization parameters:
In formula, for i-th section of heat supply steam extraction, ARiFor its energy grade quantization parameter；ΔEiDuring its energy utilization
'sVariable quantity, kJ/kg；ΔHiFor the enthalpy variable quantity during its energy utilization, kJ/kg；T0For environment temperature, K；ΔSi
For the changes of entropy amount during its energy utilization, kJ/kgK；QRiFor the heating load of its heat supply steam extraction, kJ；ARFor heat supply pumping
The energy grade quantization parameter of vapour；QRFor the heating load of heat supply steam extraction, kJ；
3) the weight proportion coefficient in gas-steam combined cycle system for heat and generating power is determined:
XqR=ARQR/AfQcogf
XqP=APQP/AfQcogf
In formula, XqRFor the weight proportion coefficient in system for heat loss energy；XqPFor the power of power generation consumption energy in system
Weight proportionality coefficient；AfFor the energy grade quantization parameter of fuel；APFor the energy grade quantization parameter of electric energy；QcogfFor fuel combustion
Burning, chemical energy are changed into the quantity of thermal energy, kJ；QPFor the energy for issuing electric energy, kJ；
4) final cost allocation is determined, final cost allocation result is the weight in system for heat loss energy
The ratio of proportionality coefficient and itself and the sum of the weight proportion coefficient for consuming energy that generates electricity, expression formula are as follows:
In formula, βtpFor final cost allocation；Δ Q is total energy loss, kJ；ΔQrFor the energy for distributing to heat side
Loss, kJ.
Further, the loss that total energy loss Δ Q includes is as follows:
Δ Q=Δ (AfQcogf)+Δ(A3Q3)+Δ(AbQb)+Δ(A4Q4)+Δ(ArQr)
In formula, Δ (AfQcogf) it is the energy loss of natural gas in combustion；Δ(A3Q3) it is flue gas in gas turbine
The energy loss of acting process；Δ(AbQb) be waste heat boiler in energy loss；Δ(A4Q4) it is that steam in steam turbine does merits and demerits
The energy loss of journey；Δ(ArQr) it is energy loss of the heat supply steam extraction to heat user transportational process, unit is kJ.
By total energy loss Δ Q according to XqRWith XqPRatio distribution heat supply side and power generation side:
Δ Q=Δ Qr+ΔQp
In formula, Δ QpFor the energy loss for distributing to power generation side, kJ.
Further, based on the angle of thermodynamic cycle, the Maximum Value of mechanical work, therefore arrange the energy grade amount of electric energy
Change coefficient APIt is 1；What is contained due to fuel is chemical energy,Value and Lower heat value are not much different, therefore the grade system of fuel
Number AfIt is also contemplated that being the largest, it is determined as 1.
The present invention combines two aspects of quality and quantity of energy, from energy grade to determine that one kind has
Specific theoretical foundation, promotes energy cascade comprehensive utilization, and consuming energy according to its quality calculates and relatively easy, comprehensively considered combustion gas-steaming
Thermoelectricity load combination condition in the cascaded utilization of energy relationship and operational process of vapour combined cycle under specific operating condition, can rationally divide
With fuel cost to for two aspect of heat and generating power, reference frame is provided to formulate heat supply and generating price.
Detailed description of the invention
The following further describes the present invention with reference to the drawings.
Fig. 1 is cost allocation variation diagram under the conditions of G100-M50L35；
Fig. 2 is cost allocation variation diagram under the conditions of G100-H55L35；
Fig. 3 is cost allocation variation diagram under the conditions of G100-H55M55；
Fig. 4 is Gas-steam Combined Cycle heat, electric coproduction of energy cascade utilization process schematic.
Each label in figure: Af, fuel energy grade quantization parameter；Qcogf, fuel combustion, chemical energy is changed into thermal energy
Quantity；Δ(AfQcogf), the energy loss of natural gas in combustion；Δ(A3Q3), flue gas is in gas turbine acting process
Energy loss；Δ(AbQb), the energy loss in waste heat boiler；Δ(A4Q4), steam steam turbine acting process energy damage
It loses；Δ(ArQr), energy loss from heat supply steam extraction to heat user transportational process.
Symbol used herein: AR, heat supply steam extraction energy grade quantization parameter；AP, electric energy energy grade quantization parameter；
QR, heat supply steam extraction heat；QP, issue electric energy energy；Δ Q, total energy loss；ΔQr, distribute to heat supply side energy damage
It loses；ΔQp, distribute to the energy loss of power generation side；βtp, cost allocation.
Specific embodiment
The present invention is used for the Computation for apportionment side of the heat supply of Gas-steam Combined Cycle cogeneration units and fuel used to generate electricity cost
Method, the specific steps are as follows:
1) according to unit practical operation situation, steam Property parameter handbook is consulted, determines the value of parameter needed for calculating, packet
Include environment temperature, enthalpy, entropy and the heating load of each section of heat supply steam extraction, combustion engine and the generated energy of steam turbine etc.；
2) as shown in figure 4, in Gas-steam Combined Cycle cogeneration units, natural gas is generated in combustion chambers burn
Flue gas, flue gas enter gas turbine band movable vane piece rotary electrification, and the flue gas for finishing function enters waste heat boiler for heat energy transfer to steaming
In vapour, steam enters steam turbine acting power generation, and some vapor is drawn to heat user.
3) assume that unit shares n sections of heat supply steam extractions, determine the energy grade quantization system for the heat that i-th section of heat supply steam extraction is contained
Several and total heat supply steam extraction energy grade quantization parameters:
In formula, for i-th section of heat supply steam extraction, ARiFor its energy grade quantization parameter；ΔEiDuring its energy utilization
'sVariable quantity, kJ/kg；ΔHiFor the enthalpy variable quantity during its energy utilization, kJ/kg；T0For environment temperature, K；ΔSi
For the changes of entropy amount during its energy utilization, kJ/kgK；QRiFor the heating load of its heat supply steam extraction；ARFor heat supply steam extraction
Energy grade quantization parameter；QRFor the heating load of heat supply steam extraction；
4) the weight proportion coefficient in gas-steam combined cycle system for heat and generating power is determined:
XqR=ARQR/AfQcogf
XqP=APQP/AfQcogf
In formula, XqRFor the weight proportion coefficient in system for heat loss energy；XqPFor the power of power generation consumption energy in system
Weight proportionality coefficient；AfFor the energy grade quantization parameter of fuel；APFor the energy grade quantization parameter of electric energy；QcogfFor fuel combustion
Burning, chemical energy are changed into the quantity of thermal energy, unit kJ；QPFor the energy for issuing electric energy, unit kJ；
5) final cost allocation is determined, final cost allocation result is the weight in system for heat loss energy
The ratio of proportionality coefficient and itself and the sum of the weight proportion coefficient for consuming energy that generates electricity, expression formula are as follows:
In formula, βtpFor final cost allocation, Δ Q is total energy loss；ΔQrFor the energy damage for distributing to heat side
It loses, unit kJ.
For determination point for the heat supply of Gas-steam Combined Cycle cogeneration units and fuel used to generate electricity cost of the invention
The reasonability of booth method, by this method and traditional cost allocation comparison for calculation methods.Fig. 1~3 are certain gas-steam combined
Circulating thermoelectric coproduction unit, the unit share three bursts of heat supply steam extractions, when its rate of load condensate be 100%, environment temperature be 27.85
DEG C when, it is calculated to share ratio.Fig. 1~3 are respectively only to change high, medium and low voltage heat supply steam extraction, and in addition two bursts of steam extractions are constant
Operating condition.Cascade utilization method in figure is methodology of the invention.
Fig. 1~3 show that the calculated result for the cascade utilization method that the present invention is mentioned is in calorimetry and actual enthalpy drop method always
Between, and consider fuel gas-steam cogeneration units energy grade variation the characteristics of, i.e., electrically and thermally two kinds of energy products in energy
It is different in amount grade；The working substance steam that the heat grade that the working medium flue gas of combustion gas circulation contains is higher than steam circulation contains heat
The grade of amount；The heat-carrying matter steam that the heat grade that the working substance steam done work into steam turbine contains is higher than into heat supply network heat supply accumulates
The grade of heat content.In addition, this method has specific theoretical foundation, energy cascade comprehensive utilization can promote, consuming energy according to its quality calculates
It is again relatively easy, comprehensively consider specific operating condition in combustion gas-Steam Combined Cycle cascaded utilization of energy relationship and operational process
Under thermoelectricity load combination condition, can reasonable distribution fuel cost to for the aspect of heat and generating power two, be to formulate for heat and generating power valence
Lattice provide reference frame.
Claims (5)
1. a kind of methodology of the heat supply of Gas-steam Combined Cycle cogeneration units and fuel used to generate electricity cost, feature exist
In including the following steps:
1) according to unit practical operation situation, the value of parameter needed for calculating is determined；
2) assume unit share n sections of heat supply steam extractions, determine the energy grade quantization parameter for the heat that i-th section of heat supply steam extraction is contained with
And total heat supply steam extraction energy grade quantization parameter:
In formula, for i-th section of heat supply steam extraction, ARiFor its energy grade quantization parameter；ΔEiDuring its energy utilization
Variable quantity, kJ/kg；ΔHiFor the enthalpy variable quantity during its energy utilization, kJ/kg；T0For environment temperature, K；ΔSiFor it
Changes of entropy amount during energy utilization, kJ/kgK；QRiFor the heating load of its heat supply steam extraction, kJ；ARFor heat supply steam extraction
Energy grade quantization parameter；QRFor the heating load of heat supply steam extraction, kJ；
3) the weight proportion coefficient in gas-steam combined cycle system for heat and generating power is determined:
XqR=ARQR/AfQcogf
XqP=APQP/AfQcogf
In formula, XqRFor the weight proportion coefficient in system for heat loss energy；XqPFor the weight ratio of power generation consumption energy in system
Example coefficient；AfFor the energy grade quantization parameter of fuel；APFor the energy grade quantization parameter of electric energy；QcogfFor fuel combustion, change
Learn the quantity that can be changed into thermal energy, kJ；QPFor the energy for issuing electric energy, kJ；
4) final cost allocation is determined, final cost allocation result is the weight proportion in system for heat loss energy
The ratio of coefficient and itself and the sum of the weight proportion coefficient for consuming energy that generates electricity, expression formula are as follows:
In formula, βtpFor final cost allocation；Δ Q is total energy loss, kJ；ΔQrFor the energy damage for distributing to heat side
It loses, kJ.
2. point of Gas-steam Combined Cycle cogeneration units heat supply according to claim 1 and fuel used to generate electricity cost
Booth method, it is characterised in that the loss that total energy loss Δ Q includes is as follows:
Δ Q=Δ (AfQcogf)+Δ(A3Q3)+Δ(AbQb)+Δ(A4Q4)+Δ(ArQr)
In formula, Δ (AfQcogf) it is the energy loss of natural gas in combustion；Δ(A3Q3) it is that flue gas does work in gas turbine
The energy loss of process；Δ(AbQb) be waste heat boiler in energy loss；Δ(A4Q4) it is steam in steam turbine acting process
Energy loss；Δ(ArQr) it is energy loss of the heat supply steam extraction to heat user transportational process, unit is kJ.
3. Gas-steam Combined Cycle cogeneration units heat supply according to claim 1 or 2 and fuel used to generate electricity cost
Methodology, it is characterised in that by total energy loss Δ Q according to XqRWith XqPRatio distribute to heat supply side and power generation side:
Δ Q=Δ Qr+ΔQp
In formula, Δ QpFor the energy loss for distributing to power generation side, kJ.
4. point of Gas-steam Combined Cycle cogeneration units heat supply according to claim 1 and fuel used to generate electricity cost
Booth method, it is characterised in that the energy grade quantization parameter A of the electric energyPIt is 1.
5. point of Gas-steam Combined Cycle cogeneration units heat supply according to claim 1 and fuel used to generate electricity cost
Booth method, it is characterised in that the energy grade quantization parameter A of the fuelfIt is 1.
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Cited By (3)
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| CN112070337A (en) * | 2020-07-20 | 2020-12-11 | 国网河北省电力有限公司电力科学研究院 | Method and device for measuring and calculating cost of thermoelectric product of heat supply unit and terminal equipment |
| CN112668110A (en) * | 2020-12-15 | 2021-04-16 | 浙江大学 | Heat supply fuel cost apportionment method of gas-steam combined cycle cogeneration unit based on process division |
| CN113394814A (en) * | 2021-06-02 | 2021-09-14 | 清华大学 | Heat and power cogeneration unit model construction method and device considering heat grade |
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